Combined thermodynamic power and cryogenic refrigeration system using binary working fluid

• US 6,161,392 A
• Filed: 10/30/1998
• Issued: 12/19/2000
• Est. Priority Date: 09/05/1997
• Status: Expired due to Fees

• Current Assignee: Jirnov, Alexei, Olga Jirnov
• Original Assignee: Jirnov, Alexei, Olga Jirnov
• Inventors: Jirnov, Alexei, Jirnov, Olga
• Primary Examiner(s): Doerrler, William
• Assistant Examiner(s): Drake, Malik N.
• Application Number:
  US09/183,845
• Time in Patent Office: 781 Days
• Field of Search: 62/87, 62/86
• US Class Current: 62/87
• CPC Class Codes: F02G 2250/03 Brayton cycles
• CPC Class Codes: F25B 9/002 characterised by the refrigerant
• CPC Class Codes: F25B 9/06 using expanders F25B9/10 takes precedence

Abstract

A combined thermodynamic power and cryogenic refrigeration system using a first and second (binary) working fluid has a low-temperature closed bottoming cycle and either a closed or open topping cycle. In the bottoming cycle a mixture of a first gas such as helium or hydrogen and a low temperature liquid such as liquefied nitrogen is isothermally compressed and then the liquid content is separated. The separated first gas is heated using heat from a second gas or ambient air expanded in the topping cycle and then the heated first gas is adiabatically expanded and supercooled while performing useful work and thereafter is mixed with the separated liquid to serve as a coolant and facilitate rejection of adiabatic heat and to supplement the cool gas/liquid fed to the compressor and thus completes the bottoming cycle. The bottoming cycle functions to cool the second gas during its compression in the topping cycle. The topping cycles are closed or open modified Brayton cycles. The closed topping cycle uses heat of the ambient air or other low temperature heat source to simultaneously produce cool refrigerated air and power and may function as a heat pump for warming cool ambient air. The open topping cycle may use a low temperature heat source, or a high temperature heat source with regeneration, to simultaneously produce power and cool refrigerated air with high thermal efficiency.

Claims

1. A method for transforming thermal energy into mechanical energy while simultaneously producing refrigerated air utilizing binary working fluids, comprising:

introducing a first gas/liquid working fluid mixture of a non-condensable first gas having high heat capacity and a low temperature liquid into a low-temperature closed bottoming cycle;

introducing a second working fluid gas into a topping cycle and compressing and expanding said second working fluid gas in said topping cycle to produce power;

isothermally compressing, isobarically heating, and adiabatically expanding said first working fluid mixture in said low-temperature closed bottoming cycle to produce a refrigerant; and

utilizing said refrigerant produced in said low-temperature bottoming cycle to cool said second working fluid gas of said topping cycle and to facilitate rejection of waste heat.

2. The method according to claim 1, wherein

said steps of isothermally compressing, isobarically heating, and adiabatically expanding said gas/liquid mixture in said low-temperature closed bottoming cycle comprises the steps of:

introducing said gas/liquid mixture into a rotary gas/liquid compressor having a rotor and isothermally compressing it therein;

separating said isothermally compressed gas/liquid mixture into a non-condensable first gas component having a low boiling temperature and high heat capacity and a liquid component;

isobarically heating said separated non-condensable gas component in a heat exchanger having a second gas as a heat source thereby cooling said second gas to produce a cool refrigerated working fluid to be used for said second working fluid gas of said topping cycle and to facilitate rejection of waste heat of said topping cycle;

discharging said isobarically heated first gas component of said first gas/liquid working fluid from said heat exchanger into a rotary gas expander having a rotor operatively connected with said rotary gas/liquid compressor rotor;

adiabatically expanding said first gas component in said rotary gas expander to simultaneously rotate said gas expander rotor and said rotary gas/liquid compressor rotor and produce useful work and thereby extract heat from said adiabatically expanded first gas component to cool it to a temperature below the boiling point of said liquid component and facilitate rejection of waste heat from said bottoming cycle;

discharging a portion of said adiabitaclly expanded cooled first gas component from said rotary gas expander into a vortex ejector/mixer; and

introducing a portion of said separated liquid component into said vortex ejector/mixer and mixing it with said expanded cool first gas component to serve as a coolant for said liquid component and to supplement said gas/liquid mixture that is introduced into said rotary gas/liquid compressor for isothermal compression.

3. The method according to claim 2, wherein

said steps of compressing and expanding said second working fluid gas in said topping cycle comprise the steps of:

drawing said cooled second working fluid gas from said heat exchanger of said bottoming cycle and introducing it into a topping cycle rotary gas compressor having a rotor and compressing it therein;

isobarically heating said compressed second gas in a topping cycle heat exchanger having a heat source and ambient air passing therethrough to cool said ambient air and produce cool refrigerated air therefrom;

discharging said isobarically heated second working fluid gas from said topping cycle heat exchanger into a topping cycle rotary gas expander having a rotor operatively connected with said topping cycle rotary gas compressor rotor and said rotary gas expander rotor and said gas/liquid compressor rotor of said bottoming cycle; and

expanding said second working fluid gas in said topping cycle rotary gas expander to simultaneously rotate said topping cycle gas expander rotor, said topping cycle gas compressor rotor and said gas expander rotor and said gas/liquid compressor rotor of said bottoming cycle to produce useful work.

4. The method according to claim 3 comprising the further steps of:

drawing a portion of cool outside air into a topping cycle rotary air compressor having a rotor connected with said topping cycle gas compressor rotor to rotate therewith and adiabatically compressing it therein;

discharging said adiabatically compressed air into expansion valve means for throttling said warm air to atmospheric pressure to produce warm air.

5. The method according to claim 2, wherein

said steps of compressing and expanding said second working fluid gas in said topping cycle comprises the steps of:

drawing said cooled ambient air from said bottoming cycle heat exchanger and introducing it into a topping cycle rotary air compressor having a rotor and compressing it therein;

isobarically heating said compressed air in a topping cycle heat exchanger having ambient air passing therethrough to cool said ambient air passing through said topping cycle heat exchanger and produce a first portion of refrigerated air therefrom;

discharging said isobarically heated and compressed air from said topping cycle heat exchanger into a topping cycle rotary air expander having a rotor operatively connected with said topping cycle rotary air compressor rotor and said gas expander and said gas/liquid compressor rotor of said bottoming cycle; and

adiabatically expanding said heated and compressed air in said topping cycle rotary air expander to simultaneously rotate said topping cycle air expander rotor and said topping cycle rotary air compressor rotor to produce useful work and thereby extract heat from said adiabatically expanded air to produce a second portion of refrigerated air therefrom.

6. The method according to claim 2, wherein

said steps of compressing and expanding said second working fluid of said topping cycle comprises the steps of:

drawing said cooled ambient air from said bottoming cycle heat exchanger and introducing it into a topping cycle rotary air compressor having a rotor and compressing it therein;

isobarically preheating said compressed air in a topping cycle heat exchanger/recuperator using waste heat;

isobarically heating said compressed and preheated air in a topping cycle combustion chamber;

discharging said isobarically heated and compressed air from said topping cycle combustion chamber into a topping cycle rotary gas expander having a rotor connected with said topping cycle rotary air compressor rotor;

adiabatically expanding said isobarically heated and compressed air in said topping cycle rotary gas expander to simultaneously rotate said topping cycle gas expander rotor and said topping cycle air compressor rotor to produce useful work;

discharging a first portion of spent expanded air from said topping cycle gas expander into said topping cycle heat exchanger/recuperator to be used as said waste heat to produce said preheated air; and

discharging a second portion of said spent expanded air from said topping cycle heat exchanger/recuperator into a thermodynamic power system utilize the remainder of waste heat.

7. A method for transforming thermal energy into mechanical energy while simultaneously producing refrigerated air utilizing binary working fluids, comprising:

introducing a first gas/liquid working fluid mixture of a non-condensable first gas having high heat capacity and a low temperature liquid into a low-temperature closed bottoming cycle;

introducing a second working fluid gas into a topping cycle and compressing and expanding said second working fluid gas in said topping cycle to produce power;

polytropically compressing, isobarically heating, and adiabatically expanding said first working fluid mixture in said low-temperature closed bottoming cycle to produce a refrigerant; and

utilizing said refrigerant produced in said low-temperature bottoming cycle to cool said second working fluid gas of said topping cycle and to facilitate rejection of waste heat.